|Numéro de publication||US2844489 A|
|Type de publication||Octroi|
|Date de publication||22 juil. 1958|
|Date de dépôt||20 déc. 1957|
|Date de priorité||20 déc. 1957|
|Numéro de publication||US 2844489 A, US 2844489A, US-A-2844489, US2844489 A, US2844489A|
|Cessionnaire d'origine||Knapsack Ag|
|Exporter la citation||BiBTeX, EndNote, RefMan|
|Citations de brevets (19), Référencé par (121), Classifications (25)|
|Liens externes: USPTO, Cession USPTO, Espacenet|
July 22, 1958 v E. GEMME'R 2,844,489
FLUIDIZED BED COATING PROCESS Filed Dec. 20, 1957 3 Sheets-Sheet 1 5 Sheets-Sheet Filed Dec. 20,- 1957.
HIS ATTORNEYS FLUIDIZED BED COATING PROCESS Erwin Gemmer, Frankfurt am Main, Germany, assignor t Knapsack-Griesheim Aktieng'esellschaft, Knapsack, near Koln, Germany, a German company Application December 20, 1957, Serial No. 704,106
6 Claims. (Cl. 117-40) The present invention relates to protective coatings and to a method and means of producing such coatings on the surfaces of articles, and the application is a continuation-in-part of United States patent applications Serial No. 427,481, filed May 4, 1954 and Serial No. 551,943, filed December 8, 1955, now abandoned.
An important object of the present invention is the production of uniform coatings which are particularly suitable for protecting the surfaces of articles which are exposed to normally destructive solvents, chemicals, or corrosive agents, or which must be electrically insulated, or which must resist mechanical abrasive or frictional wear. Some of the materials from which the articles to be coated may be made include the various metals such as steel, aluminum, zinc and other materials disclosed in my copending applicationSerial No. 551,943.
Materials which possess superior resistance to chemicals and solvents or which are electrical insulators or which are resistant to mechanical abrasive or' frictional wear often are quite expensive and -do not possess sufficient mechanical strength and rigidity for use other than as coatings in mechanical structures. Also, the very resistance to solvents andother chemicals for which these materials may be valued make them difficult: to use in the production-of coatings by common presently known methods, such as by painting or spraying in a liquid solvent or'Iliquid dispersion form.
Accordingly, itis another important object. of the present invention-to provide a new and improved process for the production of uniform coatings without the necessity for the use of liquid solvents or dispersing-agents for the coating materials. I In practicing a process of coating heated-articles by immersion. in fluidized beds of dry and pulverulent solid coatingmate'rials, it has become apparent thatsirnple-immersion in the fluidized bed often is :not suflicient to cause the formation of a cpmp era and uniform and smooth coating on thearticle which is immersed. This observationis particularly Que with respect to downwardly facing surfaces o f arjticle s.
Therefore, another importantobject of the present invention is to provide an improved process which is particularly suited for uniformly coating articles which,
during the period of immersion in the fluidized bed, have a substantial portion ofthe immersedsurfaee in a downwardly facing'positioni Articles which have a relatively plain shape as well. a's article sf with irregularor complex shapes may be advantageously coated by'the process of this invention. Some of the, articles that may be advantageously coated are set forth'he reinafter.
Other objects and advantages ofthe invention will be apparent from the following specification.
This invention is partieularly' valuable for, and applicable to, the production of coatings from high-melting high molecular weight organic polymeric thermoplastic resins suchas polyethylene and the linear" polyamides 7 generally referred toas nylons; Nylonsfwhichare .par-
2,844,489 Patented -July 22, l 958 ticularly useful are polyhexamethylene adipamide, polyhexamethylene ,sebacamide, and the polycaprolactams such as the polymer of epsiloncaprolactam. However, the uniform protective coatings of this invention may consist of practically any material which has (1) atransient decomposition point'which is reasonably higher than its melting point, and (2) a sintering temperature lower than the melting or decomposition point of the material from which the particular articles to be coated are made. I Among other coating materials which are suitable for the present purposes are most of the thermoplastic resins or those having a thermoplastic phase, and especially those which have a transient decomposition temperature which is sufliciently removed from the melting temperature thereof to permit the material to be applied to the article to be coated by melting. Specific examples of additional materials useful for this purpose arev poly styrenes, acrylic resins, bitumen such as gilsonit'e or asphalt, shellac, and wax. Various mixtures of. two or more of the above materials may also be employed for the production of coatings in accordance with the present process. In cases where one of the materials'in a coating mixture has a melting point which is substantially below i the others, the low-melting material acts somewhat as a binder and the high-melting materials as fillers. Various other filler materials may also be added to any' of the above coating materials for various purposes such as to impart desired properties or to reduce the cost of the coating materials. Examples of suitable filling materials,
below. In addition, it sholud be capable of being mixed together without appreciable packing or cohesion of the particles into larger aggregates. 1
In carrying out the coating process of this'invention the coatingmaterial, preferably in the form of pulv'erulen't' granules, is transformed into a continuously fluidized bed, by introducing at least one current of gas under pressure therein; the bed being maintained in the'fiuidized state by controlling'the flow of the'gas. The article to be coated is at least partially immersed into the fluidized bed of the coating material while the article is heated, for example by heating the article before immersion. lnorder to produce the desired uniform coating, the article" is kept in motion during the immersion period as by moving it to and fro (which includes movement in a horizontal or vertical direction). Individual particles of the coating material adhere and melt and fuse together with other particles on the hot surface of the immersed portion of the article to form a continuous coating thereon, as described more fully below. i s
A fluidized bed is, by definition, a mass of solid particles ,which exhibits the liquid-like characteristics of mobility, hydrostatic pressure, and an observable upper freeQs urface or boundary zone across which a' marked change in concentration of particles occurs. This fluidize clbed is defined as differing from a dispersed suspension because in the latter, an upper level or interface is not formed under conditions of continuous solids entrainment and uniform superficial velocity)? (This is usually observed under conditions of low solids concentration and either high fluid velocity or low solids feed rate. Thus, in general, a dispersed suspension is analogous to a vapor, whereas a fluidized bed is analogous to a liquid. One example of this condition is observed in pneumatic transport. In a vessel containing a fluidized bed a dilute suspension of entrained particles above the bed also is such a dispersed suspension, and is frequently referred to as the disperse phase while the bed itself is referred to as the dense phase) The fluidized bed is thus alternatively defined as a dense phase. These definitions are to be found in the article entitled Fluidization Nomenclature and Symbols appearing at pages 1249 and 1250 in Industrial and Engineering Chemistry, vol. 41, No. 6, June 1949.
The preheating of the article should be to a temperatureabove the sintering or melting point of the coating material. By melting point is here meant that stage wherein the coating material is sufliciently coalesced to provide a continuous coating of the article. By sintering point is here meant that stage wherein the coating material is sufliciently tacky or sticky to adhere to the surface of the article.
If required, the coating may be reinforced by repeating the above-described process of application, that is, by re-heating and re-dipping the article.
Preferred apparatus for carrying out the process will be hereinafter more fully described in conjunction with detailed reference to the accompanying drawings wherein:
Fig. l is .a side view in section, of a tank or container for holding a fluidized bed, embodying the present invention;
Fig. 2 is a generally schematic view of a treating system embodying the present invention; and
Fig. 3' is a chart showing dipping time (powder contact time). vs. thickness of coating layer when using polyethylene as the coating material in the present process at various preheat temperatures; this chart being only representative of the characteristics of the many materials which may be used.
Various types of holding means for the article may be used. For instance, it is possible to merely use a pair of tongs with which the article is manually dipped into the fluidized bed, moved to and fro or up and down, and is then withdrawn. It is also possible to use rack-s, conveyors, or othersimilar article-carrying means as described and illustrated in my copending application Serial No. 551,943.
In many instancesit is preferable to mask the article holder or portions of the .article being coated to prevent coating thereof. It has been found that a covering of various silicone resins ,which. are of a grease-like corisistency form particularly suitable masking materials.
Any gas which is reasonably inert at the temperatures and with the materials employed may be used as the gaseous medium for fiuidizing the coating material. Air is usually satisfactory and is preferred for reasons of economy; however, in order to avoid oxidation, it is sometimes preferable to use nitrogen or some other nonoxidizing gas. The pressure of the gas may vary greatly, depending on the particular shape and dimensions of the treating tank as well as on the particular type of coating material used. The pressure of the gas, however, should not exceed the point where the upper level of the fluidized bed of coating material rises above the sides of the container or where an appreciable dust cloud of the coating material is formed above the container. In fact, the maximum pressure should be such as to prevent the production of any significant quantities of dust cloud of the coating material. Generally, the minimum gas pressure will be about 7 inches water column. The supply gas pressure may be as high as about 15 atmospheres depending on the inside diameter of the gas connection. The consumption of the gas will generally be from about 70 to about 700 cubic feet per hour. It will be understood, of course, that the rate of gas flow is veryzdependent upon the size and configuration and design of the apparatus which is used for the practice of the process.
The fluidized bed should preferably be maintained at a temperature which is suflicient to prevent the accumulation of moisture in the bed. This can be conveniently accomplished by slightly raising the temperature of the gaseous medium. However, caution should be always taken to maintain the temperature of the gas and, therefore, of the fluidized bed, below the melting temperature of the coating material.
The coating material, as has been stated above, is preferably used in pulverulent form and preferably has a granular size of between about 0.001 and about 0.024 inch. Best results have been obtained with a granular size of between 0.002 and about 0.012 inch.
The period of immersion in the fluidized bed may vary with relatively wide limits depending upon the thickness of the coating desired. Depending upon the size and heat capacity of the article to be coated, the thickness of the coating desired, the powdered coating material used, and the temperature to which the article is preheated before coating, the best immersionti-me may vary from a fraction of a second up to several minutes. Generally, the time of immersion is kept below about 50 seconds, and, preferably below about 30 seconds. During this period of time, if desired, the article may be repeatedly immersed and withdrawn from the fluidized bedto observe the progress of the formation of the coating and when the coating thickness appears adequate, further immersions need not be made.
When the article is removed from the fluidized bed, it initially appears covered with a powder. After a short interval of time, however, this powder melts, or coalesces into a continuous coating due to transfer of heat from the heated article. It will be understood that it is possible to permit the article to remain in the fluidized bed for an indefinite period during which the article may'cool and the coating may solidify. If this is done, the coating will be relatively heavy and will possess a rough, powdery outer surface of powdered coating material which has not fully coalesced and is not entirely coherent to the remainder of the coating. It will be found, however, that the intermediate portions of the coating between the outermost surface and the innermost portions will possess progressively greater degrees of coalescence and that the innermost portions will be completely coalesced into a continuous covering for the article. Such a coating structure is desirable for some purposes.
If thin-walled articles are to be coated, the heat energy therein is sometimes not suflicient to cause the melting of the powder on the surface layer of the coating material; although the under-layer, or layer immediately adjacent to the article, has been melted. In such case, higher preheating temperatures can be used or the surface of the coating may be subsequently treated with a small gas torch flame or the article may be placed in an oven or heated by other means until the surface layer has been completely melted. This procedure may also be employed to completely melt the heavy coating produced when the article is permitted to cool in the fluidized bed as described at the end of the above paragraph, if desired. Only a few seconds are generally required to smooth off the surface with the flame; whereas heating time in the oven should be about 5 to 10 minutes; although this time will vary with the materials being used. When the coating material is polyethylene, a post-heating temperature range from about 250 F. to 285 F. for about 5 to 10 minutes has been found to be satisfactory. With some materials, such as the polyamides, a relatively short postheating period in a relatively hot oven is best, while with other materials, a longer=treatment period in a cooler oven is best. With still other materials, it is inadvisable toheat the article at all after coating because such heating may injure the coating and provide un- It is sometimes necessary, in order to obtain a good adhesion of the coating to the surface of the article, to clean and roughen the surfaces thereof as, for example, by means of sand or metal-grit blasting or acid etching. This is particularly true of relatively large articles having relatively complex contours. For relatively small articles which do not have any concavities and larger articles having only convex surfacesto be coated, the sandblasting step may be omitted, since there is generally a certain amount of shrinkage of the coating onto the article Ifso that a tight adhesion is automatically efiected. the surfaces of the articles to be coated are likely to be greasly or oily, they should be degreased by a proper treatment with a suitable solvent such as carbon tetrachloride.
Apparatus 10 for carrying out the process of the present invention generally includes an open-topped container 12 of suitable cross-section, which is horizontally divided into an upper and lower chamber 14 and 16,
respectively, by means of a porous partition 18. This partition, which should be pervious to the gas used but" impervious to the particles of coating material, may preferably take the form of a porous ceramic plate, although other similar structures may be advantageously used. A porous plate structure which is preferred is composed of an Alundum refractory material composed of fused alumina grains bonded together with an aluminous glass at a high firing temperature. Whether composed of this or other materials, the porous plate preferably has a gas permeability which may be defined as that which will permit the passage of, from one to fifteen cubic feet of air at 70 F. and 25 percent relative humidity through an area of one square foot and a plate thickness of one inch at a pressure differential equivalent to two inches of water in a'period of one minute. The average pore diameter of the porous 'plate should preferably be, in a range from 0.003 to 0.004 of an inch or less. Although the porous plates may be used in a wide range of thickness, when the above-mentioned Alundum refractory material or similar porous materials are used, a preferred range of'thickness is from about 0.4 to 1.2 inches and an excellent thickness has been found to be about 0.8
It is advantageous to have a container 12 in which the walls incline outwardly towardthe top, because the smaller particles tend to ascend to greater heights in the fluidized bed, and such a configuration therefore tends to produce a more uniform coating and retards the loss of the fine particles by entrainment. Other details of the container and the porous plate are shown and described in Serial No. 551,943.
The base 16 is separated from the upper portion of the tank 14 by a horizontal slot defined by upper and lower flanges 22 and 23. Bolts not shown extend through corresponding openings in these flanges to clamp the upper portion of the tank to the base 16. Nuts hold the bolts in clamped position. In the slot defined by the flanges 22 and 23 is removably positioned the ceramic filter plate 18 which may be composed of an Alundum refractory material as described above. A removable. flexible, channel-shaped shield 28 inserted in the slot around the plate 18, the upper and lower flanges of the shield being frictionally clamped between the filter plate and the respective upper and lower flanges. By this construction,
, ized material.
6 filter plates having the desired porosity for any particular job may be interchangeablyfused' in the same apparatus. The pulverulent coating material is placed on the upper surface of the partition so that the articles. to be coated can be, at least partially, immersed'therein. Thereafter, a gas under pressure, as for example, air or nitrogen, is blown into the lower chamber of the container through the pipe 20 and the valve 21 and penetrates through the porous partition into the powder, causing the powder to be converted into a continuously fluidized bed. A blower or fan may be. built into the container 12 to supply the gas. The fluidized bed behaves substantially like a fluid so that it comes into contact with all the'surfaces of the When fluidized, the individual particles become separated from one another and the bed of coating material appears to expand tooccupy a greater volume and the upper surface of the mass of coating material 26 therefore rises to an equilibrium level within the container.
It willbe seen from the following explanation, that it is very desirable that the gas should pass through the porous plate through many small, closely-spaced pores in very minute gas streams emanating from such pores.
Accordingly, it is important that there be some appreciable degree of resistance to the gas flow through every portion of the porous plate and a measurable pressure drop across the porous plate soas to assure that there is an equalization of pressure on the bottom of the plate and a resulting even flow and equal flow through all portions thereof. It willbe seen, therefore, that the many tiny. streams of gas which are flowing through the individual pores of the porous plate, when considered in combination, comprise an'upwardly moving column of gas, all of the components of which are moving upwardly at substantially uniform parallel speeds.
1 Before the article is immersed into the fluidized bed, it is preheated to a temperature above the sintering temperature but below the decomposition point of the fluid- When this preheated article is immersed intothe fluidized bed and kept in motion as described above, the fluidized powder flows into all crevices, channels, holes, grooves and the like so that every part of the article comes into contact therewith. It will be understood, of course, that if the coating is only required ona portion of the article, only that portion need be immersed.
The thickness of the coating can be largely regulated by regulation of the preheating temperatture of the article as well as regulation of the time of immersion. The relationship of these factors is illustrated for one coating material in connection with Fig. 3 which is a chart show ing the relationship between the dipping (contacting) time and the thickness of the coating layers. The curves on this chart are based on the use of polyethylene as the coating material, and it is presented as an example relating generically to any of the aforementioned coating materials. In the tests performed for the purpose of preparing this chart, the articles coated consisted of steel having a wall thickness of one-eighth of. an inch. Where thicker walls are used, the curves begin at approximately the same point but, as the contact time increases, the curves become steeper. For longer dipping times than shown on the chart, all curves asymptotically approach the horizontal. The particle size of the coating material was in the range from 200 to 400 microns. Corresponding charts for other materials show different absolute values but the same or similar characteristic curve shapes.
The best preheating temperature for coating in accordance with the process of this invention is very largely dependent upon the size and shape and thickness and heat-storage capacity of the article to be coated. If the article is small and therefore has a low heat-storage capacity, at a low preheat temperature, the heat-storage in the article will be insufficient for the purpose of melting and causing adherence of a suflicient amount of the coating material to provide a satisfactory coating. On the other hand, if the article is relatively large or has a thick cross-section so that the heat-storage capacity is high, if the article is heated to a relatively high temperature, the period of cooling of the article after coating will be unduly extended and excessive oxidation or degradation of the coating may result.
Also, the preheating temperature must obviously be related to the sintering temperature of the coating material and must exceed that temperature. For instance, for polyethylene having a melting temperature in the order of 240 F., it has been found that metal articles can be satisfactorily preheated from 300 to 570 F. or preferably in a range from 430 to 480 F. for the production of satisfactory coatings. It may be stated that the maximum possible range of preheating temperatures for the practice of the process of this invention would be as follows: thelow limit would correspond to the melting or softening point of the material which is to form the coating, and the upper limit of the temperature range would correspond to the temperature at which the article to be coated would deform or melt, or at which the article or the coating material would decompose. Other suitable temperatures, even above the decomposition temperature of the coating material are described in the copending application Serial No. 551,943.
In the procedures described in the following examples the article being coated was maintained in a to and fro motion while heated and immersed in the fluidized bed of pulverulent coating material. The effect of the to and fro motion of the article while immersed in the fluidized bed in improving the coating, particularly on downwardly facing surfaces, may be due to the formation of eddy currents in the stream of gas ascending through the fluidized bed which bring more powder into contact with such surface, or to the disruption of a possible zone of relatively stagnant gas below the surface with the same result. However, the invention is not limited to any particular theory.
As mentioned above, the process of this invention is adapted for coating articles composed of many different materials and for the application of coatings of many diflerent materials. The following examples are therefore set forth merely for the purpose of illustrating how the process may be used for various materials, without necessarily limiting the scope of the invention thereto.
Example 1 A steel plate, the dimensions of which were 7.9 inches by 15.8 inches by 0.118 inch, was coated with polyethylene. The procedure consisted of, first, preheating the workpiece in an oven at about 609 F. The preheated article was then immersed in a fluidized bed of the polyethylene for about 14 seconds. The fluidized bed consisted of pure polyethylene having a particle size of between about 0.0078 inch and 0.0157 inch. The fluidizing gas used was nitrogen, at a supply pressure of about 4 atmospheres and at a temperature of about 68 F. The thickness of the resulting coating was about 0.030 inch. This coating was absolutely free from pores, smooth and glossy. A test with an electric spark device at 25,000 volts indicated no break-down of the coating.
A workable range of preheat temperatures for the article when employing polyethylene as the coating material is from 375 to 700 F. By way of further illustration, with a metal plate having' a thickness of about 0.4 inch which is preheated to a temperature of approximately 480 F. and dipped for 40 seconds into the fluidized coating material of Example 1, a coating of a thickness of about 0.040 inch is produced. But if the preheating temperature is dropped to 390 F. and the dipping time and the coating material remain the same, a coating which is only 0.028 inch in thickness results.
Example 2 A small toothed wheel having a diameter of about 5.9 inches, and having 18 teeth with a tooth face width of about 0.40 inch, was preheated to a temperature of about 662 F. It was then immersed for about 5 seconds into a fluidized bed of high molecular weight polycaprolactam which was being fluidized by compressed air at a supply pressure of about 3.8 atmospheres. The particle size of the coating material was between about 0.002 inch to 0.0059 inch. The workpiece was then removed from the fluidized bed and subjected to a further heat treat ment, at a temperature of between about 320 F. to 356 F. for approximately 5 minutes. The resulting coating layer had a thickness of about 0.0079 inch andwas uniformly monochromatic, glossy and hard.
Example 3 An aluminum sieve plate 15.8 inches long and 4.8 inches wide and containing holes, each of which is 0.20 inch in diameter, was heated in an oven to approximately 465 F. The plate was then immersed for approximately 12 seconds in a fluidized bed consisting of polymerized methylmethacrylate particles having a size range from about 0.0012 to 0.0047 inch. This treatment resulted in a coating approximately 0.014 inch thick having an excellent surface smoothness and a brilliant appearance without the necessity for further heating.
Example 4 A steel plate, similar to that used in Example 1, was t eated in the same manner as in Example 1, except that the coating material consisted of 99.9 percent by weight polyethylene and 0.1 percent by weight carbon black. The carbon black was added for the purpose of increasing the adhesive strength of the coating. This change in coating material did not create any substantial change in the process, or in the resultant coating except that the coating was darker than when using pure polyethylene, varying from grayish black to black.
Example 5 A small grinding drum 8 inches in diameter, 4 inches in axial depth and having a wall thickness of 0.2 inch, was preheated to about 600 F. It was then immersed for about 15 seconds in a fluidized bed consisting of about 60 percent, by weight, high molecular weight polycaprolactam polyamide and about 40 percent, by weight, polyethylene. The particle size of the polyamide was between about 0.002 and 0.006 inch, while the particle size of polyethylene was between .008 and 0.012 inch. The fluidizing gas was compressed air at a supply pressure of about 4 atmospheres. The reason for the use of the mixture was because the polyamide, although it had a sufficient abrasive strength, did not have'suflicient elasticity for the re-- quired purpose. It was found that the addition of about 40 percent polyethylene resulted in a coating which had a sufficient amount of elasticity while still being resistant to damage resulting from flying abrasive particles. This coating had a thickness of about 0.02 inch and had a dull luster similar to that of a layer made of pure polyamide.
Example 6 A steel bushing 1% inches long and having an outside diameter of 1.390 inches and an inside diameter of 1.010 inches, was preheated to a temperature of about 600 F. It was then immersed, for about 4 seconds, in a fluidized bed consisting of the linear polyamide polyhexamethylene adipamide. The particles of the coating material were, in general, of 40 mesh, or in other words, small enough to pass through a 40'mesh screen. The coated article was, thereafter, subjected to a quick pass of a gas flame.
The coating produced had a thickness of approximately 0.010 inch and was very smooth, hard and slightly hazy in appearance. After cooling, the surface of air.
the coating was machined to reduce its thickness to about 0.003 inch.
A workable range of preheattemperatures when coating with'polyhexamethylene adipamide is from about 565 to800F.
' Example 7 A steel plate 3 inches by5 inches by A inch was heated to about 600 F. and was then immersedfor about 5 seconds in a fluidized bed consisting of finely divided polystyrene. The fluidizing gas used was compressed After removal from the fluidized bed the work- .piece was subjected to a temperature of about-450 F. for about 5 minutes. The coating produced had a thickness of about 0.020 inch and had a very hard, glassy,
clear appearance. i
After .the coating was completely cooled, small cracks were observed in the interior portions of the coating, adjacent the surface of the coated article. These cracks were rather uniformly spaced'and formed a grid, giving thecoating'an appearance similar to a fine-grain alligator skin. Such a coating would have utility for decorative purposes.
' Example 8 A steel plate 3 inches by 5 inches by inch was heated .to about 350 ,F. and was then immersed for about 4 seconds in a fluidized bed containing phenol formaldehyde resin powder. The particle size of the coating material was of 40 mesh.
Unlike the majority of the other examples, the article in this case was not sandblasted before treatment but was, instead, thoroughly cleaned with carbon tetrachloride. A hard, smooth coating, having a thickness ofabout 0.025 inch, was formed; This coating was relatively clear but had a yellow green cast.
Example 9 Example. 10
' A steel plate 3 inches by 5 inches by 4: inch was heated .toabout 640. Rand then immersed for about 5 seconds in a fluidized bed containing about 95 percent, by weight,
-polyhexamethylene adip'ani'ide, and about 5 percent, by
weight, molybdenum disulphide. .The particlesize of the .polyhexamethylene adiparnide was about 40 mesh,
whereas the particle size of the molybdenum disulphide was about 220v mesh. The fluidizing gasused was com- "pressedair. The coated article, after removal'from the .fluidized bed, wassubjected to a very short after-treatment with a gas Ifiarne. The thickness of the coating produced waslabout 0.007 inch and had characteristics very similar to those of the coating produced in Example 6, except thatthe molybdenum disulphide changed the color of the coating .to a light gray.
In addition to the. production of coatings, the process of..the present invention-may also be employed for the production of thin articles of the coating material as described in Serial No. 551,943 by application of the coating material toaheated mold and then stripping the coatingfrom the mold after cooling. The coating material then forms a thinself-supporting article which, of course, is no longera coating.
-Inthe prior description of the coating process of the present invention, -it was suggested that the surface of the article to be coatedshould preferably be mechanically 10 or chemically roughened, such as by sandblasting or acid etching, in order'toimprove the adherence of the coating.
;Conversely, where his desired to produce hollow articles which are formed from a coating which is stripped from a'mold member,.the mold member is preferably provided with a very smooth surface which may be highly polished in order to reduce the adhesion of the coating and permit ease in stripping the article'from the mold. High temperature releasing agents may also be applied to the mold surface or incorporated in the coating powder formulation in order to enhance the stripping characteristics.
Since the coating materials often have a higher coefficient of thermal expansion than the mold material, the adhesion of the coatingsproduced in accordance with the process of the present invention may be greatly enhanced if the coating is appliedto an exterior surface of a small article, due to the contraction of the coating on the article upon cooling. This adherence is effective even on articles which have smooth surfaces. Because of this efiect, some diflicultyis sometimes encountered in producing articles by stripping the coatings from molds if the coating is applied to the exterior of a male mold or to convex surfaces.
Thisproblem may be overcome by heating the coated heat and the absorption of water, ISO that it may be stripped fromthe mold.
The production of thin articles from the stripped coatings is illustrated by the following example:
Example 11 A steel drill. rod having a highly polished surface and a diameter of 0.457 inch was coated over about?) inches of its length, by the procedures described above with polyhexamethylene'adipamide. The drill ro d mold was preheated at 625 F. and. dipped for about 5 seconds in a bed of :the ,a'dipamide. powder, fluidized with compressed air 'atja supply pressure .of about 3 /2 atmospheres.- The particle size of the powder was about 40 mesh. The coated mold was'postheated for a very short time with a gas fiamelarid then allowed to cool in the atmosphere. The coating thickness 'was approximately 0.015 inch.
The coated mold was then boiled for several minutes in water and-the mold wasthereafter removed from the water. The-coatingwas then quickly stripped from the mold as a unit. The resulting thin cylinder of polyamide, which was closed at one end, was used as a masking can for pain'ting operations. This article Was-smooth and I continuous; that it, itdid not contain any openings.
The best mold for the purpose of producing thin selfsupportingarticles of the coating material by means of stripping the coatings from-the mold are those which do not employ predominantly convex surfaces so as to avoid the natural adh'e'rence of the coatings *due to contraction on the' mold. Thus, if a concave mold is employed in wlhichan interior surface is coated, if the surface is highly'polished,ithe coating will contract away from the mold surface .up-on cooling and the article formed of the coatand jshape and density of the particles of coating ma- 7 "teri'alj It; may be; generally stated, however, that this japparent increase in .the volume of the material will range from approximately20 percent to 120 percent of the initial v'olume. This range is particularly applicable to "the 'thermoplastic resin materials such as the nylon polylhexarn'ethylene adipamide as described in Example 6 and high molecular'weight polyethylene.
"-In general the smaller and lighter the particles, the
.- reater--wi11- bethe increase in volume upon fluidization. It -should' be understood, also, that with the finely divid ed-particles such as are described in most of the powder, even when unfiuidized, will be approximately twice the volume which would be occupied by the same material if in the form of a single, solid piece. ingly, there will be in the order of approximately a 50 percent air or gas proportion in the unfluidized mass of coating material particles before fluidization. Also, with extremely fine, fluffy particles of some materials, this proportion of gas may rise as high as 80 percent.
The articles to be coated may be easily manually dipped into the fluidized bed 14 of coating material, or if desired, suitable mechanical means may be provided for the dipping and the shaking (to and fro) movement of the immersed article.
In large-scale production, the process is preferably carried out by means of a completely conveyorized system such as illustrated in Fig. 2. In this system, a chaintype conveyor 54 having article-supporting hooks 56 on which articles 58 are suspended, is arranged to pass successively through a series of treating stations. These stations, which are schematically represented, are shown as comprising a degreasing station at 60, a sandblasting station at 62, a preheating oven at 64, a coating station at 66 and a postheating oven at 68.
The chain conveyor 54 is of the conventional type comprising a pair of parallel chains arranged on oppositely positioned sprockets, not shown, for intermittent or indexing movement around a horizontal path. Extending between the corresponding links of each chain .are rods 70. Each hook 56 is hung on a rod 70.
At the degreasing station 60 the chain conveyor passes through oppositely arranged openings in the housing 72 containing a solvent 74. After passing through the sol- 'vent, the articles 58 are conveyed to the sandblasting station 62 which comprises a sandblasting chamber 76 in -which is positioned a throwing-wheel 78 which sandblasts the articles as they pass through. Although a throwing-wheel type of abrading device has been shown 'in the drawing, this is merely for illustrative purposes,
since any type of sandblasting apparatus may be used. The conveyor, of course, passes through slots in the chamber 76 in the same manner as at station 60. The slots in the chamber 76 are provided with cover means for the slots of the type generally used in sandblasting devices.
After leaving the sandblasting station, the conveyor moves the articles through the preheating station 64 which comprises an oven 79 maintained at the required predetermined temperature which depends on the material from which the article is made as well as on the coating material and the size of the particles thereof.
After leaving the oven 79, through which it passes by means of appropriate entrance and exit slots, the conveyor moves the article into the coating station 66. At this station there is provided a tank 80 having a fluidized bed of coating material 82 therein. This container is positioned on a lifting apparatus, indicated generally at 84. This lifting device is preferably fluid-pressure actuated, i. e. pneumatic or hydraulic, and this fluid pressure system, not shown, is operated automatically, preferably through solenoid valves, not shown, which are, in turn, electrically connected to the conveyor-drive motor for synchronous actuation with the conveyor. This pressure-control system is not shown in detail'in the drawings since it may be of standard construction and, by itself, forms no part of the present invention.
The vertical movement of the fluidized bed tank is so that when an article 58 comes into position over the tank, the tank will move upwardly to the position shown in dotted outline to encompass the article which then hangs suspended from the now motionless conveyor. At this time, a lateral vibration is provided on the conveyor by means of a split ring, generally indicated at 86 to Accordtimed with the intermittent movement of the conveyor 12 produce a to and fro motion of the article immersed in the fluidized bed. This ring 86 which encompasses this portion of the conveyor path is operated by the conveyor drive-motor, not shown, in timed relationship with the movement of the conveyor and of the vertically movable fluidized bed tank 80.
After the desired period of immersion has elapsed, the
fluidized bed tank again descends to the position shown in full line in Fig. 2, the vibratory operation of the ring 86 stops, and the conveyor indexes the article, which has just been immersed, to the next position. At this next position, there are provided one or more compressed air nozzles 88 which are arranged to either continuously or intermittently direct streams of rapidly moving air at the article, in order to remove small amounts of excess powder which may adhere to portions thereof. If the operation of the nozzles 88 is continuous, they may beoperated by an independent motor or other actuating means. However, if the operation is an intermittent one, the control valves for the nozzles are preferably of the solenoid type and are actuated by the conveyor drivemotor in timed relationship with the movement of the conveyor.
Further movement of the conveyor carries the coated article into the housing 90 of postheating oven 68. This oven 68 is similar to preheating oven 64 and is also maintained at a desired predetermined temperature. Of course, if no postheating is necessary, oven 68 may be omitted or the operation of oven 68 can be dispensed with. In such case, it is allowed to remain inoperative and the conveyor merely passes through, commencing the cooling portion of the cycle as described below. The preheating and postheating ovens 64 and 68 may be of the hot air variety, deriving heat from electrical heating coils, or the burning of a fuel such as gas or fuel oil, or other conventional means. It will be appreciated, of course, that radiant heatingor induction heating or other specialized heating systems may be advantageously employed for this purpose.
After leaving the postheating oven, and before unloading, the articles may be permitted to remain on the conveyor until they cool and the coating solidifies. In some cases it is desirable, and not harmful to the coating, to accelerate the cooling step by quenching the articles in a liquid such as water or in a refrigerated atmosphere.
The various indexing movements of the conveyor are preferably varied according to the treatments. Since some steps of the process require a greater length of time than others, the speed of the conveyor must be so adjusted that a sufficient time is spent at each treating station. In the case of a long treating step, as at the preheating or postheating stations, the article will be in operative position at all times during its stay at such station. On the other hand, where the opertaion is relatively rapid, as at the sandblasting station or the coating station, the article will remain out of operative position or the treating apparatus will remain inoperative for a time sufiicient to correlate it with the oven treatment. The oven treatment may be considerably shortened by making the ovens of great length so that a proportionally greater portion of the travel of the conveyor will be through the ovens and, therefore, there need be less stopping of the conveyor.
The duration of the various portions of the cycle of operation of the apparatus disclosed in Fig. 2 are preferably 2 to 5 seconds; coating5 to 30 seconds; transition from preheating to coatingas short as possible, preferably 2 to 5 seconds; coating-5 to 20 seconds; transition from coating to excess powder removal15 to 60 seconds; excess powder removal5 to 15 seconds; transition from excess powder removal to postheating-l5 to 60 seconds; postheatingup to 10 minutes; cooling-30 to 60 minutes.
Although the system, described above, may be operated with a single conveyor speed, it may be desirable to have tainer.
13 portions of the cycle and at faster-speedsinthe rapid portions of the cycle. Such multiple speed systems may beachievedin alnumber of ways; as for example, byusing a free-hanging primary conveyor such as shown in Fig. 2,
during the first stages of the operation, and then using secondary pusher conveyors to advancethe various portions of the primary conveyor at the various desired speeds.
' iInstead of making the operation an intermittent one, it
statioinsf 'This may-be accomplished, for example, by
making the ovensat suchlengtli that the speed of travel of the conveyorthrough thedistance covered by the oven will Y coincide with the required heating time.
In such a continuous operation, instead of having the stationary and-thisportionof the conveyor is formed to provide movement of the articles into and out of the con- To perform-this operation most efficiently, the containershould beinthe form of avat havingoutwardly vide the required immersion time. The path of travel of the conveyor through the fluidized bed should be arranged correspondingly.
This invention is applicable to awide diversity of differ; eut.products. In order to demonstrate theutility of the some instances, the name of a single machine or a category;
of .m'achines'is indicated, and it .is' to beunderstood that -suchnames are meant to indicate that variouscomponents and parts of such machinery may be coated by this process. Products in which such coatings are found to beuseful are as follows. p 7
Applications in the chemical field include pump's,valves, racks forholdingparts in liquid chemicalbaths'fsuch as plating baths, foodhanfdling machinery such as conveyor 'chutes and pastry dough pickupnfi ngers, laboratory equipment, storage and shipping containers,'-probesarid anodes made of materials such as magnesium and copper for chemical reaction tests (the coating shielding the sides of the probe to permit reaction at the ends only) and immersion heater tubes for chemical baths.
In the electrical field, suitable articles include transformer components, dynamo electric machines and parts such as rotors and stators for providing slot insulation prior to insertion of the windings, electrical conductors, battery boxes and other parts, welding electrodes, radar and radio components, connectors of the solderless type, magnetic cores and laminations, ceramic printed circuits, switch components, and lighting fixtures,
Notable applications in home appliances include radio and television cabinets and chassis, vacuum cleaners, refrigerator components including ice cube trays, shelves and racks, dishwashers and clothes washer components, such as impellers, balance rings, and shelves and racks.
Building supplies such as the following may be advantangeously coated: water heater and softening tanks, metal parts, window hardware, frames and sashes, panels and doors, bathroom and kitchen fixtures such as soap dishes, towel racks, etc., plumbing parts and fittings, and door hinge pins.
Machinery components and mechanical elements that may be coated include gear blanks and gears, sleeve bearings, and other bearings, cams and cam followers, wheels for vehicles and other machines such as machine tools and electric switch gear, metal springs, and bobbins, spindles and other textile machine components, particularly parts which physically engage the textile filaments "fluidized bed container vertically'movable, the container is -sloping sides and'a flat bottom and having alength suffi cient t-o correspond with-thespeed of the conveyor to proand threads, conveyor parts such as hooks, chains, links,
writers, calculators and computors, sieves, tachometer cables, fountain pen caps, ink cartridges, and other parts,
metal arch supports, metal stays, buckles and other small parts for clothing, oil well drilling, pumping and pipe .line equipment, bicycle parts, parts formed from sintered is fpossible't'o have a continuous cycle of operation; Inr10 powdered metal, sewing machine parts, automobile parts, such asair spring pistons and parts, highway signs and guard rails, marine parts and hardware such as propellers, anchors and outboard motor components and the like, handles for wrenches, scissors, screw drivers, and other hand tools and appliances.
Obviously many modifications and variations of. the present invention are possible in the light of the above teachings. It is, therefore, to be understood that within thescope of the appended claims the invention may be practiced otherwise than as specifically described.
1. The process. of forming a layer of material on a surface of an. article which comprises forming a fluidized bed consisting of a dense phase bounded by an upper free surface bypassing a distributed ascending current of gas at a predetermined pressure through a mass of solid,
pulverulent, layer-forming material containing particles therein which sinter when heated, immersing the article surface in said dense phase while said article is heated toa temperature below the deterioration temperature of the .article but at least as high as the sintering temperature .of said particles, moving said article surface to. and fro while 'it is immersed thereby to produce a uniform layer of said material. on said surface, and cooling the'article. a
' 2. .The :process of coating an article which comprises forming .a fluidized bed consisting of a dense phase bounded by an upper free surface by passing a distributed ascending current of gas at a predetermined pressure through coating material consisting at least in part of a mass of solid, pulverulent material which has a melting point lower than the deterioration point of the article, heating thearticle to a temperature which lies between -the'melting point and the decomposition point of the pulverulent material and below the deterioration point of the article, immersing the heated article in said dense phase for a predetermined period of time while moving the article to and fro thereby to produce a uniform layer of said pulverulent material on the surface of said article and then removing the article from said dense phase to cause the heat of the article to coalesce the pulverulent material in the layer.
3. The process of forming a layer of material on a surface of an article which comprises forming a fluidized bed consisting of a dense phase bounded by an upper free surface by passing a distributed ascending current of gas at a predetermined pressure through a mass of solid, pulverulent, layer-forming material containing particles therein which sinter when heated, said predetermined pressure being such as to effect a distributed flow of said gas through said dense phase while maintaining a zone above said upper free surface free of significant quantities of said material in dispersed suspension so that substantially all of said material remains in said dense phase, immersing the article surface in said dense phase while said article is heated to a temperature below the deterioration temperature of the article but at least as high as the sintering temperature of said particles, moving said article surface to and fro while it is immersed thereby to produce a uniform layer of said material on said surface, and cooling the article.
4. The process of forming a layer of material on a surface of an article which comprises forming a fluidized bed consisting of a dense phase bounded by an v 15 upper free surface by passing a distributed ascending current of gas at a predetermined pressure through a mass of solid, pulverulent, layer-forming material containing particles therein which sinter when heated, immersing the article surface in said dense phase while said article is heated to a temperature below the deterioration temperature of the article but at least as high as the sintering temperature of said particles, moving said article surface to and fro while it is immersed thereby to produce a uniform layer of said material on said surface, then withdrawing the article from the dense phase, heating the article to improve the coating adhering thereto, and cooling the article.
5. The process of forming a layer of material on a surface of an article which comprises forming a fluidized bed consisting of a dense phase bounded by an upper free surface by passing a distributed ascending current of gas at a predetermined pressure through a mass of solid, pulverulent, layer-forming material containing particles therein which sinter when heated, immersing the article surface in said dense phase while said article is heated to a temperature below the deterioration temperature of the article but at least as high as the sintering temperature of said particles, moving said article surface to and fro while it is immersed thereby to produce a uniform layer of said material on said surface, then withdrawing the article from the dense phase and removing excess coating material on the outer surface of the coating layer having deficient coherence to the underlying portions of the layer by exposure to a rapidly moving current of gas, and cooling the article.
6. The process of forming a layer of material on a surface of an article which comprises forming a fluidized bed consisting of a dense phase bounded by an upper free surface by passing a distributed ascending current of gas at a predetermined pressure through a mass of solid, pulverulent, layer-forming material consisting essentially of discrete solid particles in a solid, pulverulent carrier, said carrier having a melting point which is lower than the temperature of the article while immersed, said discrete particles being incapable of melting at the temperature of said article, immersing the article surface in'saiddense phase while said article is heated to a temperature below the deterioration temperature of the article but at least 16 as high as the melting temperature of said carrier, moving said article surface to and fro while it is immersed thereby to produce a uniform layer of said .material on said surface, and cooling thearticle.
References Cited in the file of this patent. I
UNITED STATES PATENTS 468,810 Leach Feb. 16, 1892 1,256,000 Fairburn Feb. 12, 1918 1,534,846 Fraser et al. Apr. 21, 1925 2,059,983 Dent et al. Nov. 3, 1936 2,135,081 Kaplan Nov. 1, 1938 2,342,661 Gunnell Feb. 29, 1944 2,395,157 Work et al. Feb. 19, 1946 2,399,717 Arveson May 7, 1946 2,414,625 Abramse et al. Ian. 21, 1947 2,496,070 Selsky Jan. 31, 1950 2,520,658 Rheem et al. Aug. 29, 1950 2,600,253 Lutz June 10, 1952 2,648,609 Wurster Aug. 11, 1953 2,654,925 Ensign et a1 Oct. 13, 1953 2,661,307 Foster Dec. 1, 1953 2,719,093 Voris Sept. 27, 1955 2,728,686 Borushko Dec. 27, 1955 2,729,194 Jones Jan. 3, 1956 FOREIGN PATENTS 700,177 Great Britain Nov. 25, 1953 OTHER REFERENCES British Plastics, vol. 23, No. 255, August 1950, pp. 56-59.
Fraser et al.: Artificial Strom of Air-Sand Floats Coal on its Upper Surface, Leaving Refuse to Sink, Coal Age, vol. 29, No. 9, Mar. 4, 1926, pp. 325, 326, 327.
Parent et al.: Fluidizing Processes, Chemical Engineering Progress, vol. 43, No. 8, August 1947, pp. 429-434.
Levaet al.: Introduction to Fluidization, Chemical Engineering Progress, vol. 44, No. 7, July 1948, pp. 511 and 512.
Gemmer: Der Heutige Stand -des Kunstoif-spritzens and Pulversinterns, Industrice-Anzeiger, Jahrgang, No. 12, Feb. 10, 1953, pp. 141-143.
UNITED STATES PATENT OFFICE CERTIFICATE OF CORRECTION Patent No. 2,844,489 July 22, 1958 Erwin Gemmer It is hereby certified that error appears in the printed specification of the above numbered patent requiring correction and that the said Letters Patent should read as corrected below.
Column 5, line 23 for "greasly" read greasy column 10, line 49, for "that it" read that is; column 12, line 54, for "opertaion" read operation line 63, the paragraph beginning with "The duration" strike out all to and including "30 to 60 minutes." in line '71, and insert instead i--- The duration of the various portions of the cycle of operation of the apparatus disclosed in Fig, 2 are preferably as follows: Preheating-up to 30 minutes; transition from preheating to coating-as short as possible, preferably 2 to 5 seconds; coating-5 to 30 seconds; transition from coating to excess powder removal -l5 to 60 seconds; excess powder removal-*5 to 15 seconds; transition from excess powder-removal to postheating -l5 to 60 seconds; postheating- -up to 10 minutes; cooling-3O to 60 minutes. column 13, line 65, for "metal" read meter column 16, line 33, list of references cited, under "OTHER REFERENCES" for "Artificial Strom" read v Artificial Storm line 43, for "Industrioeqlnzeiger" read Industrie -Anzeiger SEAL At'tcet? KARL E ROBERT c. WATSON Attestiug Oflicer Commissioner of Patents
|Brevet cité||Date de dépôt||Date de publication||Déposant||Titre|
|US468810 *||9 avr. 1891||16 févr. 1892||Brick-mold sander|
|US1256000 *||24 nov. 1917||12 févr. 1918||Diamond Match Co||Splint-impregnating means for match-machines.|
|US1534846 *||11 mai 1923||21 avr. 1925||Fraser Thomas||Process of separating loosely-mixed materials|
|US2059983 *||27 juin 1932||3 nov. 1936||Gen Plastics Inc||Method of coating abrasive particles|
|US2135081 *||13 juil. 1937||1 nov. 1938||Richards Chemical Works Inc||Soaking silk yarns|
|US2342661 *||28 janv. 1942||29 févr. 1944||Robert W Gunnell||Manufacture of capsules|
|US2395157 *||8 janv. 1943||19 févr. 1946||Metal & Thermit Corp||Coated strand material|
|US2399717 *||1 nov. 1941||7 mai 1946||Standard Oil Co||Production of dust coated materials|
|US2414625 *||15 juil. 1944||21 janv. 1947||Socony Vacuum Oil Co Inc||Process of impregnating lime particles with carbon|
|US2496070 *||31 déc. 1946||31 janv. 1950||Albert Selsky||Method of making flock coated articles|
|US2520658 *||5 janv. 1948||29 août 1950||Rheem Mfg Co||Method of galvanizing cylindrical tanks|
|US2600253 *||21 janv. 1949||10 juin 1952||Dorr Co||Fertilizer manufacture|
|US2648609 *||21 janv. 1949||11 août 1953||Wisconsin Alumni Res Found||Method of applying coatings to edible tablets or the like|
|US2654925 *||23 juin 1950||13 oct. 1953||Ford Motor Co||Precision casting process|
|US2661307 *||19 janv. 1949||1 déc. 1953||Westinghouse Electric Corp||Process for applying a completely polymerizable thermosetting resinous composition to an electrical member|
|US2719093 *||3 juin 1952||27 sept. 1955||William H Voris||Methods of applying plastic coatings|
|US2728686 *||23 déc. 1952||27 déc. 1955||Harding Mfg Company||Method for coating objects|
|US2729194 *||19 nov. 1954||3 janv. 1956||Dow Chemical Co||Apparatus for dusting plastic film and like sheet material|
|GB700177A *||Titre non disponible|
|Brevet citant||Date de dépôt||Date de publication||Déposant||Titre|
|US2969038 *||5 mars 1958||24 janv. 1961||Michigan Chrome And Chemical C||Fluidized bed apparatus|
|US2974059 *||20 déc. 1957||7 mars 1961||Knapsack Ag||Fluidized bed coating process|
|US2974060 *||18 juil. 1958||7 mars 1961||Polymer Corp||Fluidized bed coating method|
|US2981631 *||13 nov. 1957||25 avr. 1961||Polymer Corp||Fluidized bed coating method for forming a foam|
|US2987413 *||23 mars 1959||6 juin 1961||Polymer Corp||Process and apparatus for producing continuous coatings|
|US3001228 *||8 janv. 1959||26 sept. 1961||G & A Lab Inc||Coating and pelletizing of fusible materials|
|US3002231 *||6 juin 1958||3 oct. 1961||Phillips Petroleum Co||Molding process|
|US3004861 *||12 janv. 1956||17 oct. 1961||Polymer Corp||Methods and apparatus for applying protective coatings|
|US3016875 *||11 déc. 1958||16 janv. 1962||United States Steel Corp||Apparatus for coating pipe|
|US3019126 *||24 mars 1959||30 janv. 1962||United States Steel Corp||Method and apparatus for coating metal strip and wire|
|US3028251 *||20 nov. 1956||3 avr. 1962||Polymer Corp||Method of coating an article with a powdered resin composition and method of making the composition|
|US3032816 *||7 nov. 1957||8 mai 1962||Polymer Corp||Coating process and apparatus|
|US3036338 *||8 janv. 1959||29 mai 1962||G & A Lab Inc||Coating and pelletizing of fusible materials|
|US3063860 *||20 déc. 1957||13 nov. 1962||Knapsack Ag||Fluidized bed coating method and apparatus|
|US3074808 *||19 oct. 1959||22 janv. 1963||Phillips Petroleum Co||Method and apparatus for coating the interior of a pipe|
|US3078177 *||28 déc. 1959||19 févr. 1963||Phillips Petroleum Co||Fluidized bed coating process, article, and composition|
|US3081699 *||22 déc. 1958||19 mars 1963||Gulko Arnold G||Thermal reproduction|
|US3090696 *||10 sept. 1956||21 mai 1963||Knapsack Ag||Fluidized bed coating process for coating with thermosetting materials|
|US3093510 *||24 mars 1958||11 juin 1963||Polymer Processes Inc||Coating method and apparatus|
|US3097958 *||10 juin 1958||16 juil. 1963||Chain Belt Co||Fluidized coating machine|
|US3099493 *||2 févr. 1961||30 juil. 1963||Indevco Ltd||Supports for aerating particulate materials|
|US3099498 *||6 mai 1960||30 juil. 1963||Shell Process Inc||Method and apparatus for manufacturing resin coated core sand|
|US3099583 *||25 avr. 1960||30 juil. 1963||Polymer Corp||Device for masking and supporting an article|
|US3102043 *||10 août 1959||27 août 1963||Fluidized bed coating method|
|US3102823 *||11 août 1959||3 sept. 1963||Shell Oil Co||Fluidized bed coating process employing an epoxy resin, and process for preparing said resin|
|US3106769 *||1 août 1958||15 oct. 1963||Westinghouse Electric Corp||Magnetic cores hermetically sealed within metal core boxes|
|US3132967 *||3 nov. 1961||12 mai 1964||Rheem Mfg Co||Method and apparatus for applying a material to an object|
|US3136651 *||22 nov. 1961||9 juin 1964||United States Steel Corp||Method of coating metal with vinyl resin|
|US3138483 *||11 janv. 1960||23 juin 1964||Polymer Processes Inc||Apparatus for coating interior of hollow body|
|US3140195 *||18 juil. 1958||7 juil. 1964||Polymer Corp||Process for providing a coated surface|
|US3144354 *||10 mars 1960||11 août 1964||Keuffel & Esser Co||Electrographic printer|
|US3148077 *||17 févr. 1961||8 sept. 1964||Rhodiatoce S P A||Method of coating with powdered cellulose acetate|
|US3155545 *||27 févr. 1961||3 nov. 1964||Rheem Mfg Co||Apparatus for external coating of objects|
|US3161530 *||10 août 1959||15 déc. 1964||Minnesota Mining & Mfg||Coated pipe and process|
|US3167442 *||24 mai 1961||26 janv. 1965||Internat Protected Metals Inc||Method of forming a resin coating on metal|
|US3167454 *||24 déc. 1959||26 janv. 1965||Zenith Radio Corp||Fluidized-bed type of coating apparatus|
|US3178308 *||7 sept. 1960||13 avr. 1965||Pfaudler Permutit Inc||Chemical vapor plating process|
|US3183113 *||20 févr. 1962||11 mai 1965||Knapsack Ag||Fluidized bed coating process and apparatus|
|US3184325 *||1 mai 1961||18 mai 1965||Phillips Petroleum Co||Coating metal with an aminophenol or aminoalkylphenol treated polyolefin powder|
|US3185131 *||24 oct. 1960||25 mai 1965||Gen Motors Corp||Apparatus for coating articles in a fluidized bed|
|US3186860 *||13 nov. 1956||1 juin 1965||Phillips Petroleum Co||Process for coating surfaces|
|US3190845 *||30 janv. 1961||22 juin 1965||Cook Paint & Varnish Co||Coal tar coating composition|
|US3199491 *||20 mars 1961||10 août 1965||Degussa||Apparatus for coating one surface of a strip by a fluid bed sintering procedure|
|US3226245 *||5 févr. 1958||28 déc. 1965||Polymer Corp||Coating method and apparatus|
|US3231946 *||28 déc. 1962||1 févr. 1966||Prec Metalsmiths Inc||Apparatus for forming ceramic shell molds|
|US3233584 *||18 juil. 1958||8 févr. 1966||Polymer Corp||Coating process and apparatus|
|US3240744 *||19 oct. 1961||15 mars 1966||Pennsalt Chemicals Corp||Use of fusion aids in fluidized bed coating techniques|
|US3248253 *||13 juin 1963||26 avr. 1966||Sames Sa De Machines Electrost||Electrostatic transfer method and apparatus for coating articles with a fluidized composition|
|US3254625 *||31 mars 1960||7 juin 1966||Cecil W Armstrong||Apparatus for producing a fluidized bed of pulverant material|
|US3257224 *||26 déc. 1962||21 juin 1966||Azoplate Corp||Method and apparatus for developing electrostatic images|
|US3261707 *||21 oct. 1963||19 juil. 1966||Emerson Electric Co||Stator coating|
|US3262420 *||21 mars 1963||26 juil. 1966||Galvarplast S N C||Coating and oven system including work handling means|
|US3264131 *||11 mai 1964||2 août 1966||Polymer Corp||Process for fusion coating and materials used therein|
|US3264371 *||13 mars 1959||2 août 1966||Polymer Corp||Fluidized bed coating process and product|
|US3282249 *||6 août 1957||1 nov. 1966||Polymer Corp||Apparatus for coating filamentary metal article|
|US3295494 *||16 avr. 1959||3 janv. 1967||Internat Protected Metals Inc||Fluidized bed apparatus for coating the interior of hollow body|
|US3305900 *||29 oct. 1964||28 févr. 1967||Archer Daniels Midland Co||Liquidless foundry molding process|
|US3309217 *||18 juil. 1963||14 mars 1967||Polymer Corp||Coating method and apparatus|
|US3311085 *||10 mai 1965||28 mars 1967||Smith Millard F||Apparatus for coating objects|
|US3338863 *||26 déc. 1957||29 août 1967||Polymer Corp||Powdered coating compositions and the method for their application|
|US3347692 *||26 août 1964||17 oct. 1967||Dow Chemical Co||Method of coating articles with graft copolymers of polypropylene and acrylic acid|
|US3366503 *||23 janv. 1967||30 janv. 1968||Eagle Picher Ind Inc||Process of embedding flock in a polyethylene substrate|
|US3379174 *||1 avr. 1964||23 avr. 1968||Gen Electric||Apparatus for applying a coating onto a localized region of the inside of a hollow article|
|US3396699 *||21 oct. 1966||13 août 1968||Anaconda Wire & Cable Co||Continuous coating apparatus|
|US3409456 *||4 déc. 1963||5 nov. 1968||Mansfield Sanitary Inc||Method and apparatus for dusting mold cores|
|US3410709 *||22 sept. 1965||12 nov. 1968||Scholven Chemie Ag||Method of producing a polyethylene coating on a metal|
|US3419409 *||3 avr. 1967||31 déc. 1968||Polymer Corp||Process for coating|
|US3440078 *||16 mars 1966||22 avr. 1969||Polymer Corp||Holding and masking device|
|US3453354 *||27 déc. 1965||1 juil. 1969||Wallace & Tiernan Inc||Methods of manufacturing ion-exchange membranes|
|US3459578 *||18 oct. 1965||5 août 1969||Rhone Poulenc Sa||Method of coating bodies by rotation|
|US3481756 *||2 mars 1965||2 déc. 1969||Celanese Corp||Method of coating with an oxymethylene polymer|
|US3496002 *||22 avr. 1966||17 févr. 1970||Chemische Werke Witten Gmbh||Process for coating metal with aromatic polyamides|
|US3507251 *||28 mars 1968||21 avr. 1970||Schlumberger Technology Corp||Coating apparatus|
|US3510337 *||26 janv. 1967||5 mai 1970||Gen Motors Corp||Method of plasma spraying of tetrafluoroethylene - hexafluoropropylene copolymer|
|US3514309 *||19 juil. 1967||26 mai 1970||Celanese Corp||Coating process|
|US3518153 *||3 mai 1966||30 juin 1970||American Biltrite Rubber Co||Embossed floor material|
|US3532530 *||11 déc. 1967||6 oct. 1970||Eastman Kodak Co||Textured coating method|
|US3536516 *||15 sept. 1967||27 oct. 1970||Shell Oil Co||Fluidized bed process for coating articles with polylactones|
|US3541043 *||26 avr. 1967||17 nov. 1970||Gen Electric||Method of dry blending an agglomerated material with a powdered material|
|US3544351 *||30 sept. 1968||1 déc. 1970||Celanese Corp||Method for coating an article with an oxymethylene polymer and product thereof|
|US3592100 *||9 mai 1968||13 juil. 1971||Hubbell Inc Harvey||Binding screw having electrically insulated head|
|US3617327 *||29 déc. 1966||2 nov. 1971||Johns Manville||Method and apparatus for applying a coating material|
|US3619231 *||16 juin 1969||9 nov. 1971||Anchor Post Prod||Continuous metal coating process with fusible pulverulent materials|
|US3660136 *||23 nov. 1970||2 mai 1972||Gen Electric||Method of coating slotted articles|
|US3728776 *||19 avr. 1971||24 avr. 1973||Defazio L||Epoxy coating of refurbished balls|
|US3905937 *||9 nov. 1973||16 sept. 1975||Du Pont||Color concentrates|
|US3925570 *||19 sept. 1972||9 déc. 1975||Aeg Elotherm Gmbh||Method of coating metallic material onto a metallic substrate|
|US3934973 *||20 sept. 1971||27 janv. 1976||Allied Chemical Corporation||Finely divided colorants|
|US3959525 *||24 juin 1974||25 mai 1976||Gte Sylvania Incorporated||Method of coating photoflash lamp|
|US3968280 *||28 juin 1974||6 juil. 1976||Standard Oil Company||Polyolefins/polycarbonamide powder compositions suitable for the production of continuous coating on substrates such as glass or metal|
|US3985097 *||31 déc. 1974||12 oct. 1976||Acf Industries, Incorporated||Apparatus for coating workpieces with a plastic material|
|US4035528 *||4 déc. 1975||12 juil. 1977||Standard Oil Company (Indiana)||Coating substrate with polyolefin/polycarbonamide powder compositions|
|US4061835 *||25 juin 1976||6 déc. 1977||Standard Oil Company (Indiana)||Process of forming a polypropylene coated substrate from an aqueous suspension of polypropylene particles|
|US4186223 *||9 juin 1977||29 janv. 1980||Hoover Universal, Inc.||Process for coating a wire spring and evaluating previous heat treat of said wire spring|
|US4218362 *||17 nov. 1977||19 août 1980||Fuji Photo Film Co., Ltd.||Powder marking agent and marking method|
|US4271113 *||30 juil. 1979||2 juin 1981||Alza Corporation||Process for forming a passageway in an osmotic device|
|US4288468 *||18 juin 1979||8 sept. 1981||Siemens Aktiengesellschaft||Process for encapsulating electrical components by vortex sintering|
|US4338878 *||26 nov. 1980||13 juil. 1982||United Technologies Corporation||Fluidized bed with sloped aperture plate|
|US4397702 *||21 janv. 1982||9 août 1983||Johnson Controls, Inc.||Fabrication of non-conductive charged sensing probe unit|
|US4486641 *||21 déc. 1981||4 déc. 1984||Ruffini Robert S||Inductor, coating and method|
|US6395345 *||30 oct. 1998||28 mai 2002||Soerensen Frede||Coating material and application methods therefor|
|US6797066 *||21 mars 2002||28 sept. 2004||Kabushiki Kaisya Yoshino Kosakujo||Apparatus and method for powder coating|
|US8162645||24 févr. 2010||24 avr. 2012||Linares Miguel A||Apparatus for forming a polymer based part utilizing an assembleable, rotatable and vibratory inducing mold exhibiting a downwardly facing and pre-heated template surface|
|US8372478||15 juil. 2010||12 févr. 2013||Grace Engineering Corp.||Method for powder coating and decorative printing|
|US8778461||9 janv. 2013||15 juil. 2014||Grace Engineering Corp.||Method for powder coating and decorative printing and related product|
|US9771969||16 mars 2012||26 sept. 2017||Jtekt Corporation||Method of manufacturing torque transmission shaft and vehicle steering apparatus|
|US20030201561 *||15 avr. 2003||30 oct. 2003||Linares Miguel A.||Heating and particulate drawing process and assembly for aggregating plasticized granules in adhering fashion to an exposed face of a heated tool or part|
|US20060120929 *||23 nov. 2004||8 juin 2006||Patrick Ward||Quartz gas discharge lamp providing photocatalytic oxidation|
|US20100008749 *||8 juil. 2008||14 janv. 2010||Caterpillar Inc.||Modular paint line including an immersion station|
|US20100132610 *||10 févr. 2010||3 juin 2010||Linares Miguel A||Process and assembly for creating a rigid plastic part within a rotatable mold|
|US20100143605 *||10 févr. 2010||10 juin 2010||Linares Miguel A||Method for forming a three-dimensional polymer base|
|US20100148388 *||24 févr. 2010||17 juin 2010||Linares Miguel A||Apparatus and related process for forming a polymer based part utilizing an assembleable, rotatable and vibratory inducing mold exhibiting a downwardly facing and pre-heated template surface|
|US20130062033 *||18 juin 2012||14 mars 2013||LaempeReich Corporation||Method of dry coating sand cores|
|DE1224426B *||12 mars 1960||8 sept. 1966||Knapsack Ag||UEberzugsmasse zum Wirbelsintern|
|DE3237829A1 *||12 oct. 1982||28 avr. 1983||Northern Telecom Ltd||Wirbelschicht-aufbau|
|EP3020992A2||16 mars 2012||18 mai 2016||Jtekt Corporation||Method of manufacturing torque transmission shaft and vehicle steering apparatus|
|EP3020993A2||16 mars 2012||18 mai 2016||Jtekt Corporation||Method of manufacturing torque transmission shaft|
|WO2001082449A1 *||7 mars 2001||1 nov. 2001||General Electric Company||Powder coated generator field coils and related method|
|WO2012128213A1||16 mars 2012||27 sept. 2012||Jtekt Corporation||Manufacturing method for drive shaft and vehicle steering device|
|WO2013079655A3 *||30 nov. 2012||9 janv. 2014||Technische Universität Hamburg-Harburg||Method for producing a composite material, the composite material and the use of the composite material for producing specific products|
|WO2017092737A1 *||26 sept. 2016||8 juin 2017||Schaeffler Technologies AG & Co. KG||Process for producing an encoder|
|Classification aux États-Unis||427/184, 264/DIG.510, 118/57, 118/66, 118/309, 427/190, 118/421, 427/185, 118/423, 118/317, 427/201, 968/302, 425/DIG.200, 118/72, 118/58, 36/77.00R|
|Classification internationale||B05D1/24, H02K15/12, C09D5/46|
|Classification coopérative||Y10S264/51, Y10S425/02, B05D1/24, H02K15/12|
|Classification européenne||H02K15/12, B05D1/24|